Table 2.
C-source | qs (g g−1 h−1) | (mol Cmol−1) | YX/S (Cmol Cmol−1) | C-balance | Metabolites | rp (U L−1 h−1) per pulse | Price (€ kg−1) |
---|---|---|---|---|---|---|---|
Glucose (batch) | 0.059 | 0.53 | 0.498 | 1.03 | Acetate (3.0 g L−1) Ethanol (0.6 g L−1) |
6.2 | |
Glucose | 0.048 | 0.93 | 0.004 | 0.94 | Ethanol (0.3 g L−1) | 4.2 | 40 |
Sorbitol | 0.037 | 0.94 | 0.002 | 0.94 | nd | 4.8 | 20 |
Mannose | 0.051 | 0.93 | 0.008 | 0.94 | ethanol (1.0 g L−1) | 4.7 | 2,000 |
Fructose | 0.048 | 0.90 | 0.036 | 0.94 | nd | 2.2 | 62 |
Maltose | 0.006 | 0.93 | 0.014 | 0.94 | nd | 5.4 | 252 |
Glycerol | 0.023 | 1.04 | 0.011 | 1.05 | nd | 4.3 | 26 |
Lactic acid | 0.005 | 1.04 | 0.000 | 1.04 | nd | 0.5 | 24 |
q s specific substrate uptake rate, and Y X/S yields of CO2 and biomass, C-balance sum of and YX/S which should ideally give 1.0, r p volumetric productivity per pulse and nd none determined.